2015
DOI: 10.1016/j.fuproc.2014.10.031
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Syngas production by partial oxidation of methane in a microchannel reactor over a Ni–Pt/La0.2Zr0.4Ce0.4Ox catalyst

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Cited by 33 publications
(9 citation statements)
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“…CH4 can be converted into added value products either in two steps, via synthesis gas [9], or directly to C2 hydrocarbons in one step. Pyrolysis [10,11], partial oxidation [12,13], dry [14,15] and steam reforming [16] constitute CH4 valorization processes of great commercial interest [17].…”
Section: Introductionmentioning
confidence: 99%
“…CH4 can be converted into added value products either in two steps, via synthesis gas [9], or directly to C2 hydrocarbons in one step. Pyrolysis [10,11], partial oxidation [12,13], dry [14,15] and steam reforming [16] constitute CH4 valorization processes of great commercial interest [17].…”
Section: Introductionmentioning
confidence: 99%
“…However, the Ni-based catalysts often suffer from sintering of the Ni particles as well as the coke formation on Ni surface in this process. Most efforts have been made on improvement of anti-sintering and -coke Ni-based catalyst, for instance, by adding promoters (alkali, alkali earth, and rare earth metal oxides) or/and utilizing different supports (Al 2 O 3 , ZrO 2 , SiO 2 , La 2 O 3 and Y 2 O 3 ) [8][9][10][11]. The formation of 'hotspots' in the catalyst bed is considered as the one of the main causes for the Ni-sintering and carbon deposition [12].…”
Section: Introductionmentioning
confidence: 99%
“…The oxygen of CeO 2 may be involved in the oxidation of CO to C x particles. The introduction of CeO 2 accelerates the diffusion of O to PtO, but the O from PtO is not sufficient , .…”
Section: Resultsmentioning
confidence: 99%